Dielectric heat-transfer fluid

ABSTRACT

Provided is a use of a vegetable oil high in monounsaturates as dielectric and heat-transfer fluid in a device for the generation, storage, conversion and/or distribution of electrical energy.

This application is a Continuation of U.S. application Ser. No. 12/748,891, filed Mar. 29, 2010, which claims the benefit of U.S. Provisional Application No. 61/164,074, filed Mar. 27, 2009, the entire content which is hereby incorporated by reference.

FIELD OF THE INVENTION

The present invention relates to the field of dielectric heat-transfer fluids, in particular dielectric fluid made from vegetable oils for use in, e.g. liquid filled transformers.

BACKGROUND OF THE INVENTION

Electrical transformers typically have windings of conducting wire which must be separated by a dielectric (i.e. non-conducting) material. Usually the coils and dielectric material are immersed in a fluid dielectric heat transfer medium to insulate the conductor and to dissipate heat generated during operation. The heat-transfer medium must act as a dielectric as well. In a typical arrangement, cellulosic and/or aramid paper or board is used as the dielectric material. The cellulosic/aramid material is wrapped around the conducting wire, and used to separate the windings dielectrically, and may also be used as a structural support for the windings or other elements such as the cores. The fluid heat-transfer medium is typically an oil, which may be, for example mineral oil or a sufficiently robust vegetable oil.

During use of the transformer, the dielectric material and heat-transfer fluid are subjected to significant electromagnetic fields and significant variations of temperature and power surges and breakdowns. Over time, the relatively extreme conditions can lead to failure of the dielectric material and deterioration of the heat-transfer fluid. Deterioration leads to power loss due to dielectric loss, and may eventually lead to discharges and catastrophic failure of the transformer causing major pollution and/or fires. The dielectric and heat-transfer fluid can furthermore be directly and indirectly degraded by oxygen migration and water formation or ingression in the transformer.

Mineral oil generally shows excellent dielectric and heat-transfer behaviour, however, dielectric heat-transfer fluids are used in enormous quantities, (i.e. several hundreds of thousands of metric tons per year). The public becomes increasingly sensitive to environment and safety concerns around transformer units, and they are therefore subject to more and more stringent regulations. Many heat-transfer fluids currently used (such as mineral oil) pose a serious concern since they are flammable and do not biodegrade within reasonable time frame or simply not at all. Fluids coming from “bio” (i.e. living) sources are increasingly being seen as future fluids for those purposes. For example, U.S. Pat. Nos. 6,905,638 and 7,048,875 disclose transformers using vegetable oils as the heat-transfer fluid. The vegetable oil may contain chemically synthesised anti-oxidants.

A need remains for improved bio-degradable heat-transfer fluids, which are not limited to food grade oils, showing good performance over time.

SUMMARY OF THE INVENTION

In a first aspect, the invention provides a use of a soy oil as a heat-transfer dielectric fluid in a device to generate, store, convert and/or distribute electrical energy, wherein the soy oil is one in which at least 70%, preferably at least 75% of the fatty acids are C₁₄ to C₂₂ mono-unsaturated, and less than 16%, preferably less than 7%, more preferably less than 6% of the fatty acids are polyunsaturated.

In a second aspect, the invention provides a device to generate, store, convert and/or distribute electrical energy and/or optical signals, comprising:

-   -   (a) a conducting material;     -   (b) a dielectric material; and     -   (c) a heat-transfer dielectric fluid, which is a soy oil in         which at least 70%, preferably at least 75% of the fatty acids         are C₁₄ to C₂₂ mono-unsaturated, and less than 16%, preferably         less than 7%, more preferably less than 6% of the fatty acids         are polyunsaturated.

In a third aspect, the invention provides a method for preconditioning a heat-transfer dielectric fluid which is a vegetable triacylglycerol, comprising the step:

-   -   (a) exposing said fluid to a constant and uniformly distributed         electromagnetic field.

In a fourth aspect, the invention provides a dielectric material comprising an organic fibrous structure (woven or non-woven) impregnated, with at least 1 wt % of a vegetable triacylglycerol, preferably a soy oil, in which at least 70%, preferably at least 75% of the fatty acids are C₁₄ to C₂₂ mono-unsaturated, and less than 16%, preferably less than 7%, more preferably less than 6% of the fatty acids are polyunsaturated.

In a fifth aspect, the invention provides a use of a vegetable oil as a heat-transfer dielectric fluid in a device to generate, store, convert and/or distribute electrical energy, wherein the vegetable oil is a triacylglycerol having at least one hydroxy fatty acid.

In a sixth aspect, the invention provides a blended high oleic oil with an improved Df value at a constant temperature comprising:

-   -   a) a first oil in the range of 1-100 vol % that is a high oleic         soybean oil; and     -   b) a second oil in the range of 1-100 vol %; and     -   c) wherein the blended high oleic oil has an oleic acid content         of at least 70%; and wherein the Df value, at a constant         temperature, of the blended high oleic oil is improved when         compared under the same conditions to an oil not comprising the         high oleic soybean oil.

In a seventh aspect, the invention provides a blended high oleic oil with an improved Df value at a constant temperature comprising:

a) a first oil in the range of 1-100 vol % that is a high oleic soybean oil; and

b) a second oil in the range of 1-100 vol % that is a mono-alkyl ester of oleic acid; and

c) a third oil in the range of 1-100 vol %; and

d) wherein the blended high oleic oil has an oleic acid content of at least 70%; and wherein the Df value, at a constant temperature, of the blended high oleic oil is improved when compared under the same conditions to an oil not comprising the high oleic soybean oil and/or the purified esters of oleic acid.

BRIEF DESCRIPTION OF THE DRAWINGS AND SEQUENCE LISTING

FIG. 1 shows the dielectric loss factor (Df) vs temperature for comparative fluids C1 (FR3) and C2 (Biotemp) and a fluid for use according to the invention, E1 (one of the oils of the invention, VGO-B1), wherein the squares ▪ and triangles ▴ show the loss factor for comparative fluid C1 (FR3) (measured at two different times), the crosses X show the loss factor for comparative fluid C2 (Biotemp), the diamonds ♦ show the loss factor for a soybean oil for use according to the invention E1 (VGO-B1), and the filled circles ● show the loss factor for mineral oil, which is included as a reference.

FIG. 2 shows the thermo-gravimetric pattern and heat flux generated before (dotted lines) and after (solid lines) a pharmaceutical grade of Ricinoleic oil is exposed to the electromagnetic microwave treatment of Example 8.

FIG. 3 shows the thermo-gravimetric pattern and heat flux generated before (dotted lines) and after (solid lines) a commercial grade of High Oleic Sunflower oil, the comparative fluid C2, is exposed to the electromagnetic microwave treatment of Example 8.

FIG. 4 shows the thermo-gravimetric pattern and heat flux generated before (solid lines) and after (dotted lines) a commercial grade of normal soybean oil, the comparative fluid C1, was exposed to the electromagnetic microwave treatment of Example 8.

FIG. 5 shows the thermo-gravimetric pattern and heat flux generated before (solid lines) and after (dotted lines) the fluid for the use of the invention, E1, was exposed to the electromagnetic microwave treatment of Example 8.

FIG. 6 shows the thermal behaviour of untreated Kraft paper (solid line), Kraft paper imbibed with the fluid for use according to the invention (dotted lines) and Kraft paper imbibed with the fluid for use according to the invention and pre-treated with microwaves according to Example 8 (dash-dot lines).

FIG. 7A shows the Df value measured vs temperature for soy oils for use according to the invention, E2, such as “HOSO”; designated by squares and high oleic soy oil having 70%, oleic acid and 16% polyunsaturates (designated by triangles), compared to soy oils having 21% oleic acid and 61% polyunsaturates (“Cm”; designated by X's), 65% oleic acid and 20% polyunsaturates (designated by diamonds).

FIG. 7B shows the DF value measured vs temperature for soy oils for use according to the invention. The crosses designate the results for E4, having 74.36% oleic (74%);

-   -   The X's designate the results for the commodity soy oil (Cm)         having 21% oleic acid and 61% polyunsaturates.     -   The triangles designate the results for a soy oil blend having         70% oleic and 16% polyunsaturates.     -   The diamonds designate the results for a soy oil blend having         65% oleic and 20% polyunsaturates.

FIG. 8 shows the variation of Df vs oleic acid content for blended soy oils at two different temperatures (upper line: 130° C.; lower line: 90° C.).

FIG. 9 shows the dielectric loss factor (Df) vs temperature for comparative fluids C1 (FR3) and C2 (Biotemp) and two oils for use according to the invention, E2 (E1, VGO-B1) and E4 (E1, VGO-B2). wherein the squares ▪ show the loss factor for comparative fluid C1, the open triangles ▴ show the loss factor for comparative fluid C2, the diamonds ♦ show the loss factor for a soybean oils for use according to the invention E2 and E4.

FIG. 10 depicts fragment PHP19340A.

FIG. 11 depicts fragment PHP17752A.

FIG. 12 depicts plasmid PHP19340.

FIG. 13 depicts plasmid PHP17752.

FIG. 14 depicts a diagram for the production of soybean oils and soybean by-products.

SEQ ID NO: 1 sets forth the nucleotide sequence of plasmid PHP19340A.

SEQ ID NO: 2 sets forth the nucleotide sequence of plasmid PHP17752A.

SEQ ID NO: 3 sets forth the nucleotide sequence of plasmid PHP19340.

SEQ ID NO: 4 sets forth the nucleotide sequence of plasmid PHP17752.

DETAILED DESCRIPTION OF PREFERRED EMBODIMENTS

The expressions dielectric loss factor, dielectric loss value, Df value, Df, or dielectric dissipation loss are used interchangeably herein. Df and Tan delta are frequently quoted in the literature as being equivalent.

The expression “E1” is directed to all the high oleic soy oils of the invention and includes the range of the fatty acid compositions shown in Table 1 and includes without limitation the following oils: VGO-B1, VGO-B2, HOSO, the 70% oleic soybean oil shown in Table 6, E2, and E4.

Methods

Fatty acid contents of oils may be determined using gas chromatography with flame ionization detection, or reverse-phase liquid chromatography with fluorescence detection. Percentages quoted relate to relative percent expressed as %, i.e. the area under the peak of one specific fatty acid divided by the sum of the peak areas of all fatty acid in a particular sample, unless stated otherwise.

Tocopherol content of oils is determined using an HPLC method.

The inventors found that a soy oil having a relatively high (i.e. at least 70%, preferably at least 75% of the fatty acids) content of monounsaturated C₁₄ to C₂₂ fatty acids, and less than 16%, preferably less than 7%, more preferably less than 6% of polyunsaturated fatty acids, gives particularly good performance as a heat-transfer dielectric fluid.

More preferably, the soy oil for use according to the invention has at least 80% content of monounsaturated C₁₄ to C₂₂ fatty acids, particularly preferably at least 82%, preferably at least 84% content of monounsaturated C₁₄ to C₂₂ fatty acids, or at or about 85% content of monounsaturated C₁₄ to C₂₂ fatty acids.

More preferably, the soy oil for use according to the invention has less than 4% of polyunsaturated fatty acids.

In a preferred embodiment, the soy oil for use according to the invention has at least 80% content of monounsaturated C₁₄ to C₂₂ fatty acids, and less than 4% of polyunsaturated fatty acids.

More preferably, the monounsaturated fatty acids are C₁₈ monounsaturated fatty acids. Most preferably, they are oleic acid.

More preferably, the polyunsaturated fatty acids are C₁₈ fatty acids having two or three double bonds, for example C18:2 and/or C18:3.

Preferably C18:2 is less than or equal to 5%.

More preferably, the soy oil has a C18:1 content of greater than about 75% of the fatty acid moieties, and a combined C18:2 and C18:3 content of less than 7%, more preferably less than 6% of the fatty acid.

In a preferred embodiment, the soy oil has a saturated fatty acid content of less than at or about 12%, more preferably less than at or about 10%.

Higher saturated fatty acid content leads to an undesirable higher pour point, and diminished dynamic heat transfer ability.

In a particularly preferred embodiment, the soy oil has the following fatty acid content: at or about 6% C16:0, 3% C18:0, 86% C18:1, 2% C18:2 and 0-2% C18:3.

In another particularly preferred embodiment, the soy oil has the following fatty acid content: at or about 6% C16:0, 4% C18:0, 79% C18:1, 4% C18:2, 2% C18:3.

In another preferred embodiment, the soy oil has the following fatty acid content: at or about (see table below):

Fatty acid % C14:0 (myristic) 0.04 C15:0 (pentadecanoic) 0.03 C16:0 (palmitic) 6.15 C16:1 n-7 (palmitoleic) 0.10 C17:0 (margaric) 0.81 C18:0 (stearic) 3.85 C18:1 n-9 (oleic) 77.74 C18:1 (octadecenoic) 1.30 C18:2 n-6 (linoleic) 4.20 C18:3 n-3 (alpha-linoleic) 2.19 C20:0 (arachidic) 0.39 C20:1 n-9 (eicosenoic) 0.38 C20:1 n-9 (eicosadienoic) 0.40 Total polyunsaturates 6.79 C22:0 (behenic) 0.01 C24:0 (lignoceric) 0.16 Others 0.90

The soy oil preferably has a water content of less than at or about 300 ppm.

In a preferred embodiment, the soy oil additionally comprises tocopherol antioxidants. Preferably the tocopherols are present at a concentration of at least 85 mg/100 g of oil, more preferably at least 100 mg/100 g of oil, as measured by a known HPLC method. The tocopherol may be selected from naturally occurring tocopherols, in particular alpha-, beta- and gamma- and delta-tocopherols, and mixtures of these.

In a particularly preferred embodiment, the soy oil has a tocopherol content as measured by a known HPLC method of at or about 160 mg/100 g oil, and has the following fatty acid content: at or about 6% C16:0, 3% C18:0, 86% C18:1, 2% C18:2 and 2% C18:3.

In another particularly preferred embodiment, the soy oil has a tocopherol content as measured by a known HPLC method of at or about 160 mg/100 g oil, and has the following fatty acid content: at or about 6% C16:0, 4% C18:0, 79% C18:1, 4% C18:2, 2% C18:3.

The tocopherol is preferably tocopherol which is present in the soy oil or in any other vegetable oil as derived from the plant source or in natural plant extracts, NPE (i.e. as opposed to synthesized tocopherol that is added).

The soy oil may additionally comprise additives known in the art, which comprise generally less than 5 wt % of the dielectric heat-transfer fluid, for example: bactericides, metal chelators, corrosion inhibitors, antioxidants, heat-stabiliser, viscosity adjusters, pour point depressants, including natural plant extract promoting those functionalities etc.

The soy oil for use according to the invention can be blended with other fluids used for dielectric heat-transfer fluids, such as other vegetable oils, mineral oil, etc.

In a particularly preferred embodiment, the oil is derived from soybeans prepared by recombinant manipulation to give increased expression of the activity of the gene encoding oleoyl 12-desaturase.

An exemplary description of a suitable genetic manipulation in soybeans is described in U.S. Pat. No. 5,981,781 (E.I. du Pont de Nemours and Company), and is detailed below:

In soy (Glycine max) there are two genes encoding oleoyl 12-desaturase activity, one of which (GmFad 2-1) is expressed only in the developing seed (Heppard et al. (1996) Plant Physiol. 110:311-319). The expression of this gene increases during the period of oil deposition, starting around 19 days after flowering, and its gene product is responsible for the synthesis of the polyunsaturated fatty acids found in soybean oil. GmFad 2-1 is described in detail by Okuley, J. et al. (1994) Plant Cell 6:147-158 and in WO94/11516. It is available from the ATCC in the form of plasmid pSF2-169K (ATCC accession number 69092). The other gene (GmFad 2-2) is expressed in the seed, leaf, root and stem of the soy plant at a constant level and is the “housekeeping” 12-desaturase gene. The Fad 2-2 gene product is responsible for the synthesis of polyunsaturated fatty acids for cell membranes.

GmFad 2-1 was placed under the control of a strong, seed-specific promoter derived from the α′-subunit of the soybean (Glycine max) beta-conglycinin gene. This promoter allows high level, seed specific expression of the trait gene. It spans the 606 bp upstream of the start codon of the α′ subunit of the Glycine max β-congylcinin storage protein. The β-conglycinin promoter sequence represents an allele of the published β-conglycinin gene (Doyle et al., (1986) J. Biol. Chem. 261:9228-9238) having differences at 27 nucleotide positions. It has been shown to maintain seed specific expression patterns in transgenic plants (Barker et al., (1988) Proc. Natl. Acad. Sci. 85:458-462 and Beachy et al., (1985) EMBO J. 4:3047-3053). The reading frame was terminated with a 3′ fragment from the phaseolin gene of green bean (Phaseolus vulgaris). This is a 1174 bp stretch of sequences 3′ of the Phaseolus vulgaris phaseolin gene stop codon (originated from clone described in Doyle et al., 1986).

The GmFad 2-1 open reading frame (ORF) was in a sense orientation with respect to the promoter so as to produce a gene silencing of the sense GmFad 2-1 cDNA and the endogenous GmFad 2-1 gene. This phenomenon, known as “sense suppression” is an effective method for deliberately turning off genes in plants and is described in U.S. Pat. No. 5,034,323.

For maintenance and replication of the plasmid in E. coli the GmFad 2-1 transcriptional unit described above was cloned into plasmid pGEM-9z (−) (Promega Biotech, Madison Wis., USA).

For identification of transformed soybean plants the β-glucuronidase gene (GUS) from E. coli was used. The cassette used consisted of the three modules; the Cauliflower Mosaic Virus 35S promoter, the β-glucuronidase gene (GUS) from E. coli and a 0.77 kb DNA fragment containing the gene terminator from the nopaline synthase (NOS) gene of the Ti-plasmid of Agrobacterium tumefaciens. The 35S promoter is a 1.4 kb promoter region from CaMV for constitutive gene expression in most plant tissues (Odell et al. (1985) Nature 303:810-812), the GUS gene a 1.85 kb fragment encoding the enzyme β-glucuronidase (Jefferson et al. (1986) PNAS USA 83:8447-8451) and the NOS terminator a portion of the 3′ end of the nopaline synthase coding region (Fraley et al., (1983) PNAS US 80:48034807). The GUS cassette was cloned into the GmFad 2-1/pGEM-9z (−) construct and was designated pBS43.

Plasmid pBS43 was transformed into meristems of the elite soybean line A2396, by the method of particle bombardment (Christou et al., (1990) Trends Biotechnol. 8:145-151). Fertile plants were regenerated using methods well known in the art.

From the initial population of transformed plants, a plant was selected which was expressing GUS activity and which was also positive for the GmFad 2-1 gene (Event 260-05) when evaluated by PCR. Small chips were taken from a number of R1 seeds of plant 260-05 and screened for fatty acid composition. The chipped seed was then planted and germinated. Genomic DNA was extracted from the leaves of the resulting plants and cut with the restriction enzyme Bam HI. The blots were probed with a phaseolin probe.

From the DNA hybridization pattern it was clear that in the original transformation event the GmFad 2-1 construct had become integrated at two different loci in the soybean genome. At one locus (Locus A) the GmFad 2-1 construct was causing a silencing of the endogenous GmFad 2-1 gene, resulting in a relative oleic acid content of about 85% (compared with about 20% in elite soybean varieties). At locus A there were two copies of pBS43. On the DNA hybridization blot this was seen as two cosegregating bands. At the other integration locus (Locus B) the GmFad 2-1 was over-expressing.

Fourth generation segregant lines (R4 plants), generated from the original transformant, were allowed to grow to maturity. R4 seeds, which contained only the silencing Locus A (e.g., G94-1) did not contain any detectable GmFad 2-1 mRNA (when measured by Northern blotting) in samples recovered 20 days after flowering. GmFad 2-2 mRNA, although reduced somewhat compared with controls, was not suppressed. Thus the GmFad 2-1 sense construct had the desired effect of preventing the expression of the GmFad 2-1 gene and thus increasing the oleic acid content of the seed. All plants homozygous for the GmFad 2-1 silencing locus had an identical Southern blot profile over a number of generations. This indicates that the insert was stable and at the same position in the genome over at least four generations.

The soy oil is extracted from the plant source using known methods of extraction. Preferred methods of extractions are those that avoid steps that result in destruction of the natural tocopherol content. For example, it is preferred to avoid heating the oil to above 200° C. for prolonged periods, for example during deodorization steps which can be reduced or eliminated. In some instances it might be preferred to avoid hydrogenation.

It is also preferred to take fractions of the oil, which are “first” extracted meaning prior to a more exhaustive extraction of the oil out of the seed. Physical extraction is preferred over solvent extraction or any combined extraction process, which privileges the physical extraction step.

Methods for the extraction and processing of soybean seeds to produce soybean oil and meal are well known throughout the soybean processing industry. In general, soybean oil is produced using a series of steps which accomplish the extraction and purification of an edible oil product from the oil bearing seed. The oils of the invention are not limited to food-grade oils.

Soybean seeds are cleaned, tempered, dehulled, and flaked which increases the efficiency of oil extraction. Oil extraction is usually accomplished by solvent (hexane) extraction but can also be achieved by a combination of physical pressure and/or solvent extraction. The resulting oil is called crude oil. The crude oil may be degummed by hydrating phospholipids and other polar and neutral lipid complexes which facilitate their separation from the nonhydrating, triglyceride fraction (soybean oil). The resulting lecithin gums may be further processed to make commercially important lecithin products used in a variety of food and industrial products as emulsification and release (antisticking) agents. Degummed oil may be further refined for the removal of impurities; primarily free fatty acids, pigments, and residual gums. Refining is accomplished by the addition of caustic which reacts with free fatty acid to form soap and hydrates phosphatides and proteins in the crude oil. Water is used to wash out traces of soap formed during refining. The soapstock by-product may be used directly in animal feeds or acidulated to recover the free fatty acids. Color is removed through adsorption with a bleaching earth, powdered activated carbon and/or synthetic neutral resin. Which removes most of the chlorophyll and carotenoid compounds. Deodorization which is principally steam distillation under vacuum, is the last step and is designed to remove compounds which impart odor or flavor to the oil. A more detailed reference to soybean seed processing, soybean oil production and by-product utilization can be found in Erickson, 1995, Practical Handbook of Soybean Processing and Utilization, The American Oil Chemists' Society and United Soybean Board.

A second aspect of the invention provides a device to generate, store, convert and/or distribute electrical energy with or without optical signals therewith, comprising:

-   -   (a) a conducting material;     -   (b) a dielectric material; and     -   (c) a heat-transfer dielectric fluid, which is a soy oil in         which at least 70%, preferably at least 75% of the fatty acids         are C₁₄ to C₂₂ mono-unsaturated, and less than 16%, preferably         less than 7%, more preferably less than 6% of the fatty acids         are polyunsaturated.

The heat-transfer dielectric fluid used in the device of the invention may be any of the preferred oils for use in the invention described herein and any mixtures thereof.

In a preferred embodiment, the device is a transformer. Typically, the transformer will have conducting material in the form of coils or windings of conducting wire and connections (e.g. copper, aluminium, iron, steel, silver, etc.). The conducting material is wound around and covered in the dielectric material, which is typically chosen from woven or non-woven fibrous material, films and laminates, such as paper, board and/or multidimensional structures. The paper or board may be cellulosic or it may be, for example, composed of aramid fibres, preferably m-aramid fibres, polyimides, polyphenylsulfones, polyamides, polyesters (e.g. PET) and polyethylene, and combination therewith in various forms composites, laminates and tailored morphologically tailored surfaces and/or multidimensional structures and hybrids/mixtures thereof. The conducting material and the dielectric material are placed in a receptacle and the dielectric heat-transfer fluid is added to submerse or partially submerse the components. Alternatively, the dielectric material (e.g. paper or board) is impregnated with the dielectric heat-transfer fluid by absorption (“imbibing”) at various stages of its processing.

In another preferred embodiment, the dielectric heat-transfer fluid may be used for example in a generator, a capacitor, an inverter or electric motor, a switch and cables.

A third aspect of the invention is a method for preconditioning a heat-transfer dielectric fluid which is a vegetable triacylglycerol, comprising the step:

-   -   (a) exposing said fluid to a constant and uniformly distributed         electromagnetic field. The electromagnetic field may be applied         continuously or in series of constant and/or variable pulse and         relaxation sequences; repeating the exposure as often as needed.

The beneficial effect of the pre-treatment extends to all triacylglycerol dielectric heat-transfer fluids and mixtures thereof, and is not limited to the fluid used in the use according to the invention.

In a preferred embodiment, the electromagnetic field is applied in the form of microwaves.

Preferably the electromagnetic field is applied at sufficient power and for a sufficient period of time to treat the vegetable triacylglycerol to at least at or about 100° C., preferably at least at or about 120° C., but not higher than at or about 170° C., more preferably not higher than at or about 160° C. It is particularly preferred to heat the vegetable triacylglycerol to at or about 140° C.

After exposing the fluid to the electromagnetic filed, it is allowed to cool.

In one embodiment, the vegetable triacylglycerol is exposed to the electromagnetic field as a neat fluid (i.e. in a suitable receptacle), and then used as desired. In another embodiment, the vegetable triacylglycerol is first applied to an absorbent dielectric material, such as paper (e.g. cellulosic or aramid), and then the imbibed paper is subjected to the electromagnetic field including in-line processing treatment. Such in-line or off-line processing treatments will be preferably performed in a way that maximize the exposure of the oil to the electromagnetic field such as reducing gradients, mainly temperature and/or electromagnetic radiation flux, within the bulk of the material treated. Falling film transfer equipment and/or droplet chambers are suitable.

A fourth aspect of the invention is a dielectric material comprising an organic fibrous structure (e.g. woven tissues or textiles or non-woven) impregnated with at least 1 wt % of a vegetable triacylglycerol, preferably a soy oil, in which at least 70%, preferably at least 75% of the fatty acids are C₁₄ to C₂₂ mono-unsaturated, and less than 16%, preferably less than 7%, more preferably less than 6% of the fatty acids are polyunsaturated.

The vegetable triacylglycerol used for impregnation may be any of the fluids for use according to the invention described herein.

In a preferred embodiment, the organic fibrous structure is a non-woven made of cellulosic or aramid fibres, polyimides, polyphenylsulfones, polyamides, polyesters (e.g. PET) and polyethylene and combination therewith in various forms composites, laminates and tailored morphologically tailored surfaces and/or multidimensional structures and hybrids/mixtures thereof.

The vegetable triacylglycerol is preferably present at about 1 wt %-10 wt %, more preferably 10 wt % to about 50 wt %, even more preferably at or about 20 wt % to 40 wt %.

In a fifth aspect, the invention provides a use of a vegetable oil as a heat-transfer dielectric fluid in a device to generate, store, convert and/or distribute electrical energy, wherein the vegetable oil is a triacylglycerol having at least one hydroxy fatty acid. Preferably the hydroxyl fatty acid is cis-12-hydroxyoctadec-9-enoic acid, preferably having the D configuration at the chiral carbon. In a particularly preferred embodiment all of the fatty acids in the triacylglycerol are D-cis-12-hydroxyoctadec-9-enoic acid (Castor oil or ricinoleic acid) and this triacylglycerol is mixed in varying proportions with a triacylglycerol in which at least 70%, preferably at least 75% of the fatty acids are C₁₄ to C₂₂ mono-unsaturated, and less than 16%, preferably less than 7%, more preferably less than 6% of the fatty acids are polyunsaturated. Preferably, in a blend, the castor oil represents from 5 to 15% of the triacylglycerol.

The term “high oleic soybean” refers to soybean seeds that have an oleic acid content of at least 60%, 61%, 62%, 63%, 64%, 65%, 66%, 67%, 68%, 69%, 70%, 71%, 72%, 73%, 74%, 75%, 76%, 77%, 78%, 79%, 80%, 81%, 82%, 83%, 84%, 85%, 86%, 87%, 88%, 89%, 90%, 91%, 92%, 93%, 94%, and 95%. Preferred high oleic soybean oil starting materials are disclosed in World Patent Publication WO94/11516, the disclosure of which is hereby incorporated by reference.

The term “high oleic oil” refers to an oil having an oleic acid content of at least 70%, 71%, 72%, 73%, 74%, 75%, 76%, 77%, 78%, 79%, 80%, 81%, 82%, 83%, 84%, 85%, 86%, 87%, 88%, 89%, 90%, 91%, 92%, 93%, 94%, and 95%.

Useful examples of contents of polyunsaturated of the oil for the use of the present invention are less than 16%, 15%, 14%, 13%, 12%, 11%, 10%, 9%, 8%, 7%, 6%, 5%, 4%, 3%, 2%, 1%.

In a sixth aspect, the invention provides a blended high oleic oil with an improved Df value at a constant temperature comprising:

-   -   a) a first oil in the range of 1-100 vol % that is a high oleic         soybean oil; and     -   b) a second oil in the range of 1-100 vol %; and     -   c) wherein the blended high oleic oil has an oleic acid content         of at least 70%; and wherein the Df value, at a constant         temperature, of the blended high oleic oil is improved when         compared under the same conditions to an oil not comprising the         high oleic soybean oil.

Useful examples of percent volume for the oils a) and b) of the blended oil of the invention are 1%, 2%, 3%, 4%, 5%, 6%, 7%, 8%, 9%, 10%, 11%, 12%, 13%, 14%, 15%, 16%, 17%, 18%, 19%, 20%, 21%, 22%, 23%, 24%, 25%, 26%, 27, 28%, 29%, 30%, 31%, 32%, 33%, 34%, 35%, 36%, 37%, 38%, 39%, 40%, 41%, 42%, 43%, 44%, 45%, 46%, 47%, 48%, 49%, 50%, 51%, 52%, 53%, 54%, 55%, 56%, 57%, 58%, 59%, 60%, 61%, 62%, 63%, 64%, 65%, 66%, 67%, 68%, 69%, 70%, 71%, 72%, 73%, 74%, 75%, 76%, 77%, 78%, 79%, 80%, 81%, 82%, 83%, 84%, 85%, 86%, 87%, 88%, 89%, 90%, 91%, 92%, 93%, 94%, 95%, 96%, 97%, 98%, 99%, and 100%.

The amount of oil which can be used will depend upon the desired properties sought to be achieved in the resulting final blended oil product.

In a seventh aspect, the invention provides a blended high oleic oil with an improved Df value at a constant temperature comprising:

-   -   a) a first oil in the range of 1-100 vol % that is a high oleic         soybean oil; and     -   b) a second oil in the range of 1-100 vol % that is a mono-alkyl         ester of oleic acid; and     -   c) a third oil in the range of 1-100 vol %; and     -   d) wherein the blended high oleic oil has an oleic acid content         of at least 70%; and wherein the Df value, at a constant         temperature, of the blended high oleic oil is improved when         compared under the same conditions to an oil not comprising the         high oleic soybean oil and/or the purified esters of oleic acid.

Useful examples of percent volume for the oils a), b) and c) of the blended oil of the invention are 1%, 2%, 3%, 4%, 5%, 6%, 7%, 8%, 9%, 10%, 11%, 12%, 13%, 14%, 15%, 16%, 17%, 18%, 19%, 20%, 21%, 22%, 23%, 24%, 25%, 26%, 27, 28%, 29%, 30%, 31%, 32%, 33%, 34%, 35%, 36%, 37%, 38%, 39%, 40%, 41%, 42%, 43%, 44%, 45%, 46%, 47%, 48%, 49%, 50%, 51%, 52%, 53%, 54%, 55%, 56%, 57%, 58%, 59%, 60%, 61%, 62%, 63%, 64%, 65%, 66%, 67%, 68%, 69%, 70%, 71%, 72%, 73%, 74%, 75%, 76%, 77%, 78%, 79%, 80%, 81%, 82%, 83%, 84%, 85%, 86%, 87%, 88%, 89%, 90%, 91%, 92%, 93%, 94%, 95%, 96%, 97%, 98%, 99%, and 100%.

The amount of oil which can be used will depend upon the desired properties sought to be achieved in the resulting final blended oil product.

The oil b) that is a mono-alkyl ester of oleic acid can be any C₁-C₁₂alkyl ester of oleic acid. Particularly preferred are C₁-C₈alkyl esters, more preferably C₁-C₆alkyl esters, such as methyl, ethyl, propyl, butyl, pentyl and hexyl esters, both straight and branched.

The oil described herein was tested for its suitability as a heat-transfer dielectric fluid by measuring the dielectric dissipation loss, Df. Df is an important parameter to compare fluids used for dielectric insulation and/or heat transfer in the presence of electrical and/or magnetic fields.

The dielectric dissipation loss, Df, in part, represents the tendency of the fluid in an alternating electromagnetic field to depart from the ideal of a pure dielectric medium in which no energy dissipation losses would occur. The dielectric loss typically increases with the presence of impurities in the fluid, especially charged impurities, with increase in water content, with free acids and with molecular breakdown of the fluid into smaller species. Furthermore, the stability of the dielectric loss versus temperature within a representative temperature range is an insurance of a durable fluid composition exhibiting good performance over prolonged period of time (i.e. good aging behaviour).

The measurement of Df is made using ASTM D924, and is based on the superheterodyne principle.

In one aspect the soy oil or blended oil for use according to the invention preferably shows a Df of less than at or about 1.2×10⁻³ when measured at 23° C., preferably less than at or about 5.4×10⁻³ when measured at 70° C., preferably less than 9.1×10⁻³ when measured at 90° C., preferably less than at or about 1.21×10⁻² when measured at 100° C., preferably less than at or about 1.95×10⁻² when measured at 120° C., preferably less than at or about 2.32×10⁻² when measured at 130° C., and preferably, it shows a Df of less than at or about 2.32×10⁻² over a temperature range of at or about 23-130° C.

In another aspect the soy oil or blended oil for use according to the invention preferably shows a Df of less than at or about 2.5×10⁻⁴ when measured at 23° C., preferably less than at or about 2.5×10⁻³, more preferably less than at or about 1.5×10⁻³ when measured at 70° C., preferably less than at or about 5×10⁻³, more preferably less than at or about 3×10⁻³ when measured at 90° C., preferably less than at or about 7×10⁻³, more preferably less than at or about 4×10⁻³ when measured at 100° C., preferably less than at or about 2×10⁻², more preferably less than at or about 7×10⁻³ when measured at 120° C., and preferably less than at or about 2×10⁻², more preferably less than at or about 1×10⁻² when measured at 130° C. Preferably, it shows a Df of less than at or about 2×10⁻², more preferably less than at or about 1×10⁻² over a temperature range of at or about 23-130° C.

In one aspect for the use according to the invention, a blended oil may be used. Such blends are made by blending a high oleic soy oil having an oleic acid content of at least 70%, preferably at least 75% with another oil, preferably a vegetable oil. The quantity of high oleic soy oil to be added to another oil may be determined by titration: the high oleic soy oil may be added until the blended oil has a Df of less than at or about 1.2×10⁻³ when measured at 23° C., preferably less than at or about 5.4×10⁻³ when measured at 70° C., preferably less than 9.1×10⁻³ when measured at 90° C., preferably less than at or about 1.21×10⁻² when measured at 100° C., preferably less than at or about 1.95×10⁻² when measured at 120° C., preferably less than at or about 2.32×10⁻² when measured at 130° C., and preferably, it shows a Df of less than at or about 2.32×10⁻² over a temperature range of at or about 23-130° C.

The high oleic soy oil that is used for blending preferably has a polyunsaturated content of less than at or about 16%, more preferably less than at or about 7%.

In another aspect for the use according to the invention, a blended oil may be used. Such blends are made by blending a high oleic soy oil having an oleic acid content of at least 70%, preferably at least 75% with another oil, preferably a vegetable oil. The quantity of high oleic soy oil to be added to another oil may be determined by titration: the high oleic soy oil may be added until the blended oil has a Df of less than at or about 2.5×10⁻⁴ when measured at 23° C., preferably less than at or about 2.5×10⁻³, more preferably less than at or about 1.5×10⁻³ when measured at 70° C., preferably less than at or about 5×10⁻³, more preferably less than at or about 3×10⁻³ when measured at 90° C., preferably less than at or about 7 X 10⁻³, more preferably less than at or about 4×10⁻³ when measured at 100° C., preferably less than at or about 2×10⁻², more preferably less than at or about 7×10⁻³ when measured at 120° C., and preferably less than at or about 2×10⁻², more preferably less than at or about 1×10⁻² when measured at 130° C. Preferably, the blended oil shows a Df of less than at or about 0.02, more preferably less than at or about 1×10⁻² over a temperature range of at or about 23-130° C. The high oleic soy oil that is used for blending preferably has a polyunsaturated content of less than at or about 16%, more preferably less than at or about 7%.

A dynamic (natural or forced) heat transfer takes place in most electrical equipment cooled and electrically insulated with oils. The heating of a liquid filled transformer must be controlled, in large proportion by the coolant and dielectric fluid, taking into account fairly large temperature variations, between the internal hotspots and the external temperature extremes, in winter and in summer. Under good controlled conditions the transformer can be in operation for more than 30 years; but can also be quickly damaged with relatively small deviations, sometime less than 10° C., from the ideal operating temperature defined for each category of transformers and the energy transformation load for which they have been designed.

At least four important properties of the oil vary with temperature, each of them at various degrees leading to reversible or irreversible property changes in the dielectric heat-transfer fluid (oil). These properties are the density, the thermal conductivity, the dynamic viscosity (all three of which decrease with increasing temperature) and the specific heat (which increases with increasing temperature).

For an oil temperature variation from 25° C. to 85° C., it is preferred that the density change be less than at or about 5%, the conductivity change be less than at or about 3%, the heat capacity change be less than at or about 10%. The viscosity change is by far the most substantial, since it can reach 50% for the same range of temperature.

Therefore the viscosity, which contributes to the fluid mechanics via the Re number (Reynold Re=(velocity.diameter.density)/viscosity), directly impacts the fluid's heat-transfer capability, yielding a poorer heat transfer when the viscosity increases and a better one if the viscosity decreases.

EXAMPLES Example 1

Transformation of Soybean (Glycine max)

Embryo Cultures and Regeneration of Soybean Plants.

Soybean embryogenic suspension cultures are transformed by the method of particle gun bombardment using procedures known in the art (Klein et al. (1987) Nature (London) 327:70 73; U.S. Pat. No. 4,945,050; Hazel et al. (1998) Plant Cell. Rep. 17:765 772; Samoylov et al. (1998) In Vitro Cell Dev. Biol. Plant 34:8 13). In particle gun bombardment procedures it is possible to use purified 1) entire plasmid DNA or, 2) DNA fragments containing only the recombinant DNA expression cassette(s) of interest.

Stock tissue for transformation experiments are obtained by initiation from soybean immature seeds. Secondary embryos are excised from explants after 6 to 8 weeks on culture initiation medium. The initiation medium is an agar solidified modified MS (Murashige and Skoog (1962) Physiol. Plant. 15:473 497) medium supplemented with vitamins, 2, 4-D and glucose. Secondary embryos are placed in flasks in liquid culture maintenance medium and maintained for 7-9 days on a gyratory shaker at 26+/−2° C. under ˜80 μEm-2s-1 light intensity. The culture maintenance medium is a modified MS medium supplemented with vitamins, 2, 4-D, sucrose and asparagine. Prior to bombardment, clumps of tissue are removed from the flasks and moved to an empty 60×15 mm petri dish for bombardment. Tissue is dried by blotting on Whatman #2 filter paper. Approximately 100-200 mg of tissue corresponding to 10-20 clumps (1-5 mm in size each) are used per plate of bombarded tissue.

After bombardment, tissue from each bombarded plate is divided and placed into two flasks of liquid culture maintenance medium per plate of bombarded tissue. Seven days post bombardment, the liquid medium in each flask is replaced with fresh culture maintenance medium supplemented with 100 ng/ml selective agent (selection medium). For selection of transformed soybean cells the selective agent used can be a sulfonylurea (SU) compound with the chemical name, 2 chloro N ((4 methoxy 6 methyl 1,3,5 triazine 2 yl)aminocarbonyl) benzenesulfonamide (common names: DPX-W4189 and chlorsulfuron). Chlorsulfuron is the active ingredient in the DuPont sulfonylurea herbicide, GLEAN®. The selection medium containing SU is replaced every week for 6-8 weeks. After the 6-8 week selection period, islands of green, transformed tissue are observed growing from untransformed, necrotic embryogenic clusters. These putative transgenic events are isolated and kept in media with SU at 100 ng/ml for another 2-6 weeks with media changes every 1-2 weeks to generate new, clonally propagated, transformed embryogenic suspension cultures. Embryos spend a total of around 8-12 weeks in contact with SU. Suspension cultures are subcultured and maintained as clusters of immature embryos and also regenerated into whole plants by maturation and germination of individual somatic embryos.

Example 2 Genetic Material Used to Produce the High Oleic Trait

A Soybean (Glycine max) event was produced by particle co-bombardment as described in Example 1 with fragments PHP19340A (FIG. 10; SEQ ID NO: 1) and PHP17752A (FIG. 11; SEQ ID NO: 2). These fragments were obtained by Asc I digestion from a source plasmid. Fragment PHP19340A was obtained from plasmid PHP19340 (FIG. 12; SEQ ID NO: 3) and fragment PHP17752A was obtained from plasmid PHP17752 (FIG. 13; SEQ ID NO: 4). The PHP19340A fragment contains a cassette with a 597 bp fragment of the soybean microsomal omega-6 desaturase gene 1 (gm-fad2-1) (Heppard et al., 1996, Plant Physiol. 110: 311-319).

The presence of the gm-fad2-1 fragment in the expression cassette acts to suppress expression of the endogenous omega-6 desaturases, resulting in an increased level of oleic acid and decreased levels of palmitic, linoleic, and linolenic acid levels. Upstream of the gm-fad2-1 fragment is the promoter region from the Kunitz trypsin inhibitor gene 3 (KTi3) (Jofuku and Goldberg, 1989, Plant Cell 1: 1079-1093; Jofuku et al., 1989, Plant Cell 1: 427-435) regulating expression of the transcript. The KTi3 promoter is highly active in soy embryos and 1000-fold less active in leaf tissue (Jofuku and Goldberg, 1989, Plant Cell 1: 1079-1093). The 3′ untranslated region of the KTi3 gene (KTi3 terminator) (Jofuku and Goldberg, 1989, Plant Cell 1: 1079-1093) terminates expression from this cassette.

The PHP17752A fragment contains a cassette with a modified version of the soybean acetolactate synthase gene (gm-hra) encoding the GM-HRA protein with two amino acid residues modified from the endogenous enzyme and five additional amino acids at the N-terminal region of the protein derived from the translation of the soybean acetolactate synthase gene 5′ untranslated region (Falco and Li, 2003, U.S. Patent Application: 2003/0226166). The gm-hra gene encodes a form of acetolactate synthase, which is tolerant to the sulfonylurea class of herbicides. The GM-HRA protein is comprised of 656 amino acids and has a molecular weight of approximately 71 kDa.

The expression of the gm-hra gene is controlled by the 5′ promoter region of the S-adenosyl-L-methionine synthetase (SAMS) gene from soybean (Falco and Li, 2003, U.S. Patent Application: 2003/0226166). This 5′ region consists of a constitutive promoter and an intron that interrupts the SAMS 5′ untranslated region (Falco and Li, 2003). The terminator for the gm-hra gene is the endogenous soybean acetolactate synthase terminator (als terminator) (Falco and Li, 2003, U.S. Patent Application: 2003/0226166).

Example 3 Transformation and Selection for the Soybean High Oleic Event

For transformation of soybean tissue, a linear portion of DNA, containing the gm-fad2-1 gene sequence and the regulatory components necessary for expression, was excised from the plasmid PHP19340 through the use of the restriction enzyme Asc I and purified using agarose gel electrophoresis. A linear portion of DNA, containing the gm-hra gene sequences and the regulatory components necessary for expression, was excised from the plasmid PHP17752 through the use of the restriction enzyme Asc I and purified using agarose gel electrophoresis. The linear portion of DNA containing the gm-fad2-1 gene is designated insert PHP19340A and is 2924 bp in size. The linear portion of DNA containing the gm-hra gene is designated insert PHP17752A and is 4511 bp in size. The only DNA introduced into transformation event DP-305423-1 was the DNA of the inserts described above.

The transgenic plants from event DP-305423-1 were obtained by microprojectile bombardment as described in Example 1. Embryogenic tissue samples were taken for molecular analysis to confirm the presence of the gm-fad2-1 and gm-hra transgenes by Southern analysis. Plants were regenerated from tissue derived from each unique event and transferred to the greenhouse for seed production.

Example 4 Southern Analysis of Plants Containing the High Oleic Event

Materials and Methods: Genomic DNA was extracted from frozen soybean leaf tissue of individual plants of the T4 and T5 generations of DP 305423 1 and of control (variety: Jack) using a standard Urea Extraction Buffer method. Genomic DNA was quantified on a spectrofluorometer using Pico Green® reagent (Molecular Probes, Invitrogen). Approximately 4 pg of DNA per sample was digested with Hind III or Nco I. For positive control samples, approximately 3 pg (2 genome copy equivalents) of plasmid PHP19340 or PHP17752 was added to control soybean genomic DNA prior to digestion. Negative control samples consisted of unmodified soybean genomic DNA (variety: Jack). DNA fragments were separated by size using agarose gel electrophoresis.

Following agarose gel electrophoresis, the separated DNA fragments were depurinated, denatured, neutralized in situ, and transferred to a nylon membrane in 20×SSC buffer using the method as described for TURBOBLOTTER™ Rapid Downward Transfer System (Schleicher & Schuell). Following transfer to the membrane, the DNA was bound to the membrane by UV crosslinking.

DNA probes for gm-fad2-1 and gm-hra were labelled with digoxigenin (DIG) by PCR using the PCR DIG Probe Synthesis Kit (Roche).

Labelled probes were hybridized to the target DNA on the nylon membranes for detection of the specific fragments using DIG Easy Hyb solution (Roche) essentially as described by manufacturer. Post-hybridization washes were carried out at high stringency. DIG labelled probes hybridized to the bound fragments were detected using the CDP-Star Chemiluminescent Nucleic Acid Detection System (Roche). Blots were exposed to X ray film at room temperature for one or more time points to detect hybridizing fragments. The fatty Acid composition of the event was determined as described in Example 2. Oleic acid levels determined in 29 different events (T1 generation) ranged from 61.5-84.6%. Oleic acid level from one event (T4-T5 generation) ranged from 72-82%.

Example 5 Fatty Acid Contents and Compositions

Qualitative and quantitative fatty acid compositions of oils were determined using modifications of AOCS Ce 2-66 (Preparations of methyl esters of fatty acids) and AOCS Ce 1e-91 (Determination of fatty acids in edible oils and fats by capillary GLC) official methodologies as follows. Oil stocks were prepared by adding 0.5000 gm (weighed and recorded to an precision of 0.0001 g) of oil and 0.0130 g to 0.0260 g (weighed and recorded to an precision of 0.0001 g) of internal standard (tri-pentadecanoin; NuChek Prep; Elysian Minn., USA) to a 10 ml volumetric flask; the internal standard was omitted where the analysis was limited to qualitative (area %) data. Seven ml heptane was added and the stock was sonicated for 2 min to ensure full dissolution of the Internal Standard Powder (IST) powder. After cooling to room temperature the stock was brought to volume with heptane. Stocks were prepared immediately prior to analysis. Dilution series of the oils stocks were then prepared by adding 0, 50, 100, (4×150), 200, 250, and 300 ul (˜0-0.0150 g oil per tube) of the oil stock to pre-labelled tubes (glass 13×100 mm with Teflon lid inserts; VWR 53283 800 tubes, 60826-304 caps; VWR Bridgeport N.J., USA) and bringing each sample to a final volume of 300 ul with heptane. The tubes were prepared for derivatization by wrapping the threaded portions with PTFE sealant tape. Derivatization was performed as follows: The tubes were vortex mixed and 1 mL of derivatization acid stock (prepared by adding 5 mL acetyl chloride (Fluka 00990; Sigma Aldrich St Louis Mo., USA) to 50 ml ice-cold anhydrous methanol) was added. The tubes were capped tightly, re-vortex and incubated at 80° C. in a heat block for 1 hr. The tubes were cooled to room temp and 1 mL of aqueous 1M NaCl was added followed 0.5 mL heptane. The samples were vigorously vortex mixed and the phases were allowed to separate prior to transferring ˜200 uL of the upper (heptane) phase to a GC sample vial fitted with a liner (Part #225350-631SP; Wheaton, Millville N.J., USA). Samples were analyzed by GC as follows. An Agilent 6890 fitted with an Omegawax 320 (Supelco, Bellefonte Pa., USA) capillary column (30m×0.32 mm ID; 0.25 um film thickness). One ul samples were injected at a 10:1 split ratio into the GC inlet which was heated to 250° C. Hydrogen was used as the carrier gas at a linear velocity of 39 cm/sec (constant flow mode). The initial oven temperature was 160° C. for 4 min and the oven temperature was then ramped to 220° C. at 2 C./min and was then held at the final temperature for 10 min (total run time 44 min). Detection was by flame ionization and a NuChek Prep 461 Standard (1:100 dilution in heptane; NuChek Prep; Elysian Minn., USA) was used to identify peaks, by co-chromatography. All peaks with an area >0.01% were included in the analysis.

Tocopherol Analysis

Tocopherol contents were measured according to AOCS Official Method Ce 8-89 on an Agilent 1100 HPLC system fitted with a 250×4 mm Lycoshere Si 60 (5 um) analytical column and a G1321A fluorescence detector. Oil stocks, as described above, without internal standard were used for this analysis. Quantitative standards dissolved in heptane, were prepared with authentic α (alpha), β (beta), γ (gamma) and δ (delta) tocopherol standards (Supelco, Bellefonte Pa., USA). Standard concentrations were confirmed by UV-spectroscopy using the following wavelengths and extinction coefficients [α (alpha), OD292, 0.0076; β (beta) OD296, 0.0089; γ (gamma) OD298, 0.0091; δ (delta) OD298, 0.0087].

Oil quality and oxidative stability measurements

Free Fatty Acid Content

Free fatty acid contents of the oils were performed by titration using a Mettler-Toledo DL22 F&B titrator (Mettler-Toledo, Columbus Ohio, USA) according to the manufacturers protocol M345 (Acid Number of edible oils).

Peroxide Value

Peroxide values of the oils were performed by iodometric titration using a Mettler-Toledo DL22 F&B titrator (Mettler-Toledo, Columbus Ohio, USA) according to the manufacturers protocol M346 (Peroxide value in edible oils and fats).

p-Anisidine Value

p-Anisidine values were determined on oils according to AOCS official method Cd 18-90.

Oxidative Stability Index

The oxidative stability index was measured on 5.0+/−0.2 g samples of pure oil samples (with or without additives) according to AOCS official method Cd 12b-92, using an OSI-24 Oxidative Stability Instrument. Instrument control and data analysis were performed using OSI Program v8.18 and Instacal 5.33 software (Omnion, Inc, Rockland Mass., USA).

TABLE 1 Fatty acid profiles of some soy oils 16:0 18:0 18:1 18:2 18:3 % Total poly- % % % % % unsaturates Commodity Soy  8-13 2-6 18-27 51-59  6-10 57-69 Oil¹ E1, an example of 6-7 4-5 70-86  2-13 2-3  4-16 the range of High Oleic Soy Oils for use according to the invention For this table, fatty acid % relates the individual fatty acid to the sum of the five major fatty acids indicated. Other fatty acid types that are sometimes present and represent less than 3% of the total fatty acids are not considered for purposes of comparison ¹Value ranges for the five major fatty acids in commodity soy oil are taken from “The Lipid Handbook” 2nd ed., (1994) Gunstone, F. D., Harwood, J. L., Padley, F. B., Chapman & Hall. 16:0 = palmitic acid, 18:0 = stearic acid, 18:1 = oleic acid, 18:2 = linoleic acid, 18:3 = linolenic acid

Example 6 Dielectric Loss

The loss factor (Df) was measured using ASTM D924 for the dielectric heat-transfer fluids shown in Table 2, at different temperatures. Loss factor was plotted VS temperature.

The results are shown in FIG. 1, wherein the squares ▪ and triangles ▴ show the loss factor for comparative fluid C1 (measured at two different times), the crosses X show the loss factor for comparative fluid C2, the diamonds ♦ show the loss factor for a soybean oil for use according to the invention E1, and the filled circles ● show the loss factor for mineral oil, which is included as a reference.

TABLE 2 Dielectric heat-transfer fluids used for experiments Tocopherol Fatty acid composition % content Reference Fluid C16:0 C18:0 C18:1 C18:2 C18:3 mg/100 g oil C1 Envirotemp ® 10 4 23-48 34-54 1-8 140 FR3 ™ fluid (soy oil) (Cooper Industries, Inc.) C2 BIOTEMP ® (Total 84-85 10-12 0-3 46 (sunflower) saturates) Biodegradable 3-8 Dielectric Insulating Fluid (ABB, Inc.) E1 One of the 6.15 3.85 77.74 4.20 2.19 97 mg/100 ml soybean oil s (fluid for the use of the invention)

TABLE 3 Detailed fatty acid composition of dielectric heat-transfer fluid E1 used for experiments Fatty acid % C14:0 (myristic) 0.04 C15:0 (pentadecanoic) 0.03 C16:0 (palmitic) 6.15 C16:1 n-7 (palmitoleic) 0.10 C17:0 (margaric) 0.81 C18:0 (stearic) 3.85 C18:1 n-9 (oleic) 77.74 C18:1 (octadecenoic), 1.30 C18:2 n-6 (linoleic) 4.20 C18:3 n-3 (alpha-linoleic) 2.19 Total polyunsaturates 0.39 C20:0 (arachidic) 0.38 C20:1 n-9 (eicosenoic) 0.40 C20:1 n-9 (eicosadienoic) 6.79 C22:0 (behenic) 0.01 C24:0 (lignoceric) 0.16 Others 0.00

It is clear from FIG. 1 that the soybean oil for use according to the invention (E1) shows a low dielectric loss factor that stays relatively consistent with increase in temperature, whereas the other vegetable oils (C1 and C2) show significant increases in loss factor as the temperature is increased.

The results are shown in tabular form in Table 4.

TABLE 4 Df for oil E1 at various temperatures Temperature (° C.) Df 23   2 × 10⁻⁴ 70 1.4 × 10⁻³ 90 2.7 × 10⁻³ 100 3.6 × 10⁻³ 120 6.5 × 10⁻³ 130 8.1 × 10⁻³

Example 7 Breakdown Voltage

The dielectric breakdown voltage is an essential parameter to compare fluids used for dielectric insulation and/or heat exchange in the presence of electrical and magnetic fields. It is also a relevant indication of the arcing transmission characteristics of the fluid.

The dielectric breakdown voltage, measured according to ASTM D877, characterises the dielectric performance limit of the fluid, which is a bulk property giving indirect access to the ultimate voltage under which the dielectric can be used and its ability to sustain eventual voltage pulses.

The soy oil for use according to the invention (E1) has a breakdown voltage at 23° C. within the range of 57 to 66 kV. In contrast, the two comparative fluids C1 and C2 have breakdown voltages in the range of 47 to 65 kV at 25° C., i.e. significantly broader and lower. The fluid for use according to the invention (E1) is clearly superior, exhibiting better consistency versus arcing transmission as well.

Example 8 Pre-Treatment Method

The fluid for the use according to the invention (E1) as well as the two comparative fluids (C1 and C2) of a mass of 2.6 g were exposed to a commercial microwave treatment of one minute at a maximum power of 900 W. Such conditions were selected to yield a fluid temperature inferior to 200° C. and preferably lower than 160° C. in order to maintain the molecular integrity of the essential components of the fluid.

Example 9 Differential Scanning Calorimetry and Thermogravimetric Analysis

In order to demonstrate the benefit of the pre-treatment method by electromagnetic microwave exposure (Example 8), various vegetable dielectric heat-transfer fluids were subjected to differential scanning calorimetry coupled with thermogravimetric analysis, both with and without the pre-treatment.

Specific conditions and equipment references are provided below:

Equipment: 2960 SDT-CE5275 Ta Instrument (simultaneously performing DSC-TGA—differential scanning calorimetric and thermogravimetric analysis)

Test conditions:

-   -   10° C./min till 650[° C.]     -   air flow: 100 ml/min     -   air composition

N₂: 78.09%

O₂: 20.95%

Ar: 0.93%

CO₂: 0.03

FIG. 2 shows the thermo-gravimetric pattern and heat flux generated before (dotted lines) and after (solid lines) a pharmaceutical grade of Ricinoleic oil is exposed to the electromagnetic microwave treatment of Example 8.

The heat flux signal definition and their relative strength clearly show a beneficial preconditioning of the oil by the electromagnetic microwave treatment process and method therewith, as is shown for example by the sharpness of the peaks, the start and the onset temperatures after the pre-treatment.

FIG. 3 shows the thermo-gravimetric pattern and heat flux generated before (dotted lines) and after (solid lines) a commercial grade of High Oleic Sunflower oil, the comparative fluid C2, is exposed to the electromagnetic microwave treatment of Example 8.

The heat flux signal definition and their relative strength clearly show a beneficial preconditioning of the oil by the electromagnetic microwave treatment process and method therewith, as is shown by the sharpness of the peaks after the pre-treatment.

FIG. 4 shows the thermo-gravimetric pattern and heat flux generated before (solid lines) and after (dotted lines) a commercial grade of normal soybean oil, the comparative fluid C1, was exposed to the electromagnetic microwave treatment of Example 8.

The heat flux signal definition and their relative strength clearly show a beneficial preconditioning of the oil by the electromagnetic microwave treatment process and method therewith, as is shown by the sharpness of the peaks after the pre-treatment.

FIG. 5 shows the thermo-gravimetric pattern and heat flux generated before (solid lines) and after (dotted lines) the fluid for the use of the invention, E1, was exposed to the electromagnetic microwave treatment of Example 8.

The heat flux signal definition and their relative strength clearly show a beneficial preconditioning of the oil by the electromagnetic microwave treatment process and method therewith, as is shown by the sharpness of the peaks after the pre-treatment.

Note: the beneficial effect of the pre-treatment extends to all triacylglycerol dielectric heat-transfer fluids and mixtures thereof, and is not limited to the fluid used in the use according to the invention.

Example 10 Behaviour of Dielectric Heat-Transfer Fluid with Dielectric Paper

Commercially available transformer insulation Kraft paper, from Weidmann AG, Rapperswill, Switzerland, was impregnated at room temperature, via a naturally occurring imbibing process, with an amount equivalent to 30 wt % of the fluid for use according to the invention. The initial specific weight of the paper was 95 g/m².

One sample of such imbibed paper was subjected to the microwave pre-treatment method of Example 8, and a second was not.

FIG. 6 shows the thermal behaviour of untreated Kraft paper (solid line), Kraft paper imbibed with the fluid for use according to the invention (dotted lines) and Kraft paper imbibed with the fluid for use according to the invention and pre-treated with microwaves according to Example 8 (dash-dot lines).

The imbibing of the Kraft paper with the fluid for use according to the invention results in an enhancement of the thermal resistance of the paper by 20-40° C. The microwave pre-treatment results in a further enhancement by 10° C.

The impregnation can be done during the manufacture of the paper or after. The microwave treatment can be repeated as many times as needed and can be performed by exposing said fluid to a constant and uniformly distributed electromagnetic field applied continuously or in series of constant and/or variable pulse and relaxation sequences; repeating the exposure sequence as often as needed. Inventor found for example that the exposure of 7.2 g of oil of the invention to 20 cycles of 10 s 300 W-microwave pulse and 50 s relaxation were effective in preconditioning the oil without causing damage that may be provoked by prolonged higher-microwave-power exposure.

The imbibing oil can be any oil mixtures of the invention. An oil of the invention mixed with 20% of a commodity linseed oil has surprisingly shown good sealing properties that are especially valuable in sealed electrical devices of the invention, especially transformers, which tend to micro-leak with time, especially for those used for relatively long period of time, such as 20 to 30 years. The sealing nature of the oil of the blends of the invention is especially appreciated. Naturally occurring or synthesised epoxidized vegetable oil have also been found as exhibiting similar sealing effect of the insulating paper as well as at sealing interfaces.

The paper treatment with the oil of the invention and/or mixtures thereof, has valuable effect on the viscoelastic behaviour of the paper and its mechanical resistance to puncture and tearing, for example; leading to enhance paper endurance appreciated to extend the life of the electrical device, such as liquid filled transformers.

Example 12

It was found that under moderate ageing (88 hours at 170° C. in an air ventilated oven) the dynamic viscosity of a conventional commodity soy oil having about 21% monounsaturated C18/1, increased irreversibly from 60 to 180 mPa·s as measured at 23° C. Furthermore, the conventional oil showed a strong colour change from a pale yellow to a rosewood colour. This represents a 3× increase in dynamic viscosity over a relatively short period of time. Such an increase in dynamic viscosity could lead to a 25% adjustment need of the circulated volume and pressure drop compensation within a transformer.

An oil for use according to the invention, E1, was subjected to the same heat aging, and no change in dynamic viscosity was observed.

This kind property makes the oil particularly useful as a dielectric heat-transfer fluid.

Example 13

An experiment was done to determine the effect of oleic acid content on Df vs temperature behaviour.

A given amount of a low linoleic soy oil (LL) having the fatty acid composition (“FAC”) profile given in Table 6 was blended with an oil for the use of the invention, E4, of the profile given in Table 6 to produce blended oils corresponding to 70% and 65% oleic acid oil mixtures of the FAC profile given in Table 6. A commodity soy oil sample (Cm) of the FAC profile given in Table 6 served as a representative of a lower oleic oil content sample.

TABLE 6 FAC of various soy oils and blended soil oils used for Example 13. 70% 65% FAC, Relative % E2 E4 oleic oleic LL Cm C14 (Myristic) 0.04 0.04 0.04 0.05 0.07 0.07 C15 0.03 0.03 0.03 0.03 0.02 0.02 (Pentadecanoic) C16 (Palmitic) 6.15 6.26 6.68 7.12 10.37 10.27 C16:1n7 0.10 0.09 0.08 0.09 0.1 0.09 (Palmitoleic) C17 (Margaric) 0.81 0.74 0.7 0.64 0.11 0.10 C17:1 1.35 0.01 1.06 0.96 0.07 0.06 C18 (Stearic) 3.85 3.94 4.09 4.19 4.77 4.59 C18:1n9 (Oleic) 77.74 74.36 69.24 64.53 20.96 21.29 C18:1 1.30 1.17 0.89 0.9 1.44 1.43 Octadecenoic C18:2n6 (Linoleic) 4.20 8.7 12.74 17.06 57.01 53.46 C18:3n3 (alpha- 2.19 2.92 2.82 2.85 3.02 7.21 Linolenic) C20 (Arachidic) 0.39 0.37 0.37 0.36 0.35 0.35 C20:1n9 0.38 0.29 0.27 0.26 0.17 0.19 (Eicosenoic) C20:2n6 0.40 0.35 0.35 0.35 0.37 0.36 Eicosadienoic Total 6.79 11.97 15.91 20.26 60.4 61.03 polyunsaturates C22 (Behenic) 0.01 0.0 0 0 0.01 0.37 C24 (Lignoceric) 0.16 0.10 0.07 0.07 0.1 0.13 C24:1 0.00 0 0 0 0 0 Other 0.90 0.63 0.57 0.54 1.06 0.01

Samples of the oils and blends listed in Table 6 were submitted to the Df analysis as described in Example 6, measuring Df as a function of temperature, at temperatures ranging from 23 to 130° C.

FIGS. 7A and 7B show the variation of Df as a function of temperature for the oils and blended oils listed in Table 6. FIG. 7A shows oils of the invention comprising 78% oleic acid (E2,) compared to commodity oil and a 65% oleic acid blend and a 70% oleic acid blend. FIG. 7B shows oils of the invention comprising a 74% oleic acid content (E4) compared to commodity oil and a 65% oleic acid blend and a 70% oleic acid blend. In FIG. 7A the squares designate the results for E2 (“HOSO”), having 77.74% oleic acid.

The X; s in FIG. 7B designate the results for E4, having 74.36% oleic (74%);

The asteriks in FIGS. A and B designate the results for the commodity soy oil (Cm) having 21% oleic acid and 61% polyunsaturates. The triangles designate the results for a soy oil blend having 70% oleic and 16% polyunsaturates in FIGS. 7A and 7B.

The diamonds designate the results for a soy oil blend having 65% oleic and 20% polyunsaturates in FIGS. 7A and 7B.

It is clear from FIGS. 7A and 7B that the oils for use according to the invention E1 show superior behaviour over the other oils, in that the Df is lower and stays lower over the entire temperature range of 23-130° C. Furthermore, the oils of the invention E1, such as for example the 70% oleic acid blend, the oil E2 and oil E4 show less increase in Df with temperature.

The commodity soy oil Cm without antioxidants and other additives responds similarly to the commercial soy oil C1 containing traditional additives for the transformer applications.

FIG. 8 shows the variation of Df as a function of the oleic content in percent, at two temperatures (130° C., upper line, and 90° C., lower line). It can be seen from FIG. 8 that at both temperatures the Df drops as the oleic acid content increases, with a sharp decrease from at or about 65% oleic acid to at or about 70% oleic acid. The oil used for this experiment was oil E2 as an example for one of the oils of the invention.

Example 14

An additional experiment was done to measure Df as a function of temperature (according to Example 6) using two different soy oils for use according to the invention, E2 and E4, as compared with high oleic sunflower oil (84% oleic acid, 8% total polyunsaturates), and oils C1 and C2. The FAC of the oils is listed in Table 7.

TABLE 7 FAC of oils used in experiments of Example 14 High Oleic Oil E2 E4 Sunflower C1 C2 FAC, Relative % C14 (Myristic) 0.04 0.04 0.03 0.07 0.04 C15 0.03 0.03 0.01 0.02 0.01 (Pentadecanoic) C16 (Palmitic) 6.15 6.26 2.97 10.57 3.59 C16:1n7 0.10 0.09 0.07 0.09 0.09 (Palmitoleic) C17 (Margaric) 0.81 0.74 0.03 0.10 0.03 C17:1 1.35 0.01 0.06 0.06 0.05 C18 (Stearic) 3.85 3.94 2.95 4.35 2.93 C18:1n9 (Oleic) 77.74 74.36 84.21 21.38 83.81 C18:1 1.30 1.17 0.59 1.44 0.23 Octadecenoic C18:2n6 4.20 8.70 7.15 53.68 7.19 (Linoleic) C18:3n3 (alpha- 2.19 2.92 0.10 7.21 0.17 Linolenic) C20 (Arachidic) 0.39 0.37 0.26 0.33 0.27 C20:1n9 0.38 0.29 0.29 0.18 0.27 (Eicosenoic) C22 (Behenic) 0.4 0.35 0.88 0.01 0.82 C24 (Lignoceric) 0.16 0.10 0.30 0.02 0.04 C24:1 0.00 0.00 0.02 0.00 0.00 Other 0.91 0.63 0.08 0.49 0.46

The Df was measured at various temperatures according to Example 6. The results are listed in Table 8. The results clearly show that oils E2 and E4, which are soy oils for use according to the invention, show significantly lower Df's over the temperature range of 23-130° C., and show less increase in Df at high temperatures than the comparative oils. The high oleic sunflower Df data are locally just in between E4 and C1, close to C1 indicating a significant variation of the high oleic sunflower Df values within the 23 to 130 C temperature range. The high oleic sunflower without antioxidants and other additives responds similarly to the commercial high oleic sunflower C2 containing traditional additives for the transformer applications.

TABLE 8 Df for oils at various temperatures High oleic Temp C1 C2 E2 E4 sunflower 23 0.0016 0.0007 0.0002 0.0018 0.0003 70 0.0081 0.0085 0.0014 0.0021 0.006 90 0.0146 0.0166 0.0027 0.0044 0.016 100 0.0201 0.0208 0.0036 0.0059 0.0154 120 0.0287 0.0372 0.0065 0.0128 0.0296 130 0.0402 0.0524 0.0081 0.0186 0.0302

FIG. 9 shows in graphic form the dielectric loss factor (Df) VS temperature for comparative fluids C1 and C2 and for oils E2 and E4, wherein the squares ▪ show the loss factor for comparative fluid C1, the open triangles ▴ show the loss factor for comparative fluid C2, the diamonds ♦ show the loss factor for a soybean oil for use according to the invention E2 and E4, lower line E2, upper line E4. 

What is claimed is:
 1. A dielectric material comprising an organic fibrous structure impregnated with at least 10% wt of a high oleic soybean oil in which at least 75% of the fatty acids are C₁₄ to C₂₂ mono-unsaturated, less than 7% of the fatty acids are polyunsaturated, and further wherein the oil comprises tocopherol antioxidants at a concentration of at least 85 mg/100 g of oil.
 2. The dielectric material of claim 1, wherein the high oleic soybean oil has less than 6% polyunsaturated fatty acids.
 3. A blended high oleic oil comprising: a) a first oil in the range of 1-100 vol % that is a high oleic soybean oil; and b) a second oil in the range of 1-100 vol %; wherein the blended high oleic oil has an oleic acid content of at least 70% and a polyunsaturated fatty acid content of less than 16%, wherein the blended high oleic oil comprises tocopherol antioxidants at a concentration of at least 85 mg/100 g of oil; and wherein the Df value, at a constant temperature, of the blended high oleic oil is improved when compared under the same conditions to a comparable oil not comprising the high oleic soybean oil.
 4. The blended high oleic oil of claim 3, having a Df of less than about 1.2×10⁻³ when measured at 23° C.
 5. The blended high oleic oil of claim 3, having a Df of less than about 5.4×10⁻³ when measured at 70° C.
 6. The blended high oleic oil of claim 3, having a Df of less than about 9.1×10⁻³ when measured at 90° C.
 7. The blended high oleic oil of claim 3, having a Df of less than about 1.21×10⁻² when measured at 100° C.
 8. The blended high oleic oil of claim 3, having a Df of less than about 1.95×10⁻² when measured at 120° C.
 9. The blended high oleic oil of claim 3, having a Df of and less than about 2.32×10⁻² when measured at 130° C.
 10. The blended high oleic oil of claim 3, having a Df of less than 2.32×10⁻² over a temperature range of about 23-130° C.
 11. The blended high oleic oil of claim 3, having a Df of less than about 2.5×10⁻⁴ when measured at 23° C.
 12. The blended high oleic oil of claim 3, having a Df of less than about 1.5×10⁻³ when measured at 70° C.
 13. The blended high oleic oil of claim 3, having a Df of less than about 3×10⁻³ when measured at 90° C.
 14. The blended high oleic oil of claim 3, having a Df of less than about 4×10⁻³ when measured at 100° C.
 15. The blended high oleic oil of claim 3, having a Df of less than about 7×10⁻³ when measured at 120° C.
 16. The blended high oleic oil of claim 3, having a Df of and less than about 1×10⁻² when measured at 130° C.
 17. The blended high oleic oil of claim 3, having a Df of less than 0.01 over a temperature range of about 23-130° C.
 18. A blended high oleic oil with an improved Df value at a constant temperature, the blended high oleic oil comprising: a) a first oil in the range of 1-100 vol % that is a high oleic soybean oil; and b) a second oil in the range of 1-100 vol % that is a mono-alkyl ester of oleic acid; and c) a third oil in the range of 1-100 vol %; wherein the blended high oleic oil has an oleic acid content of at least 80% and additionally comprises tocopherol antioxidants at a concentration of at least 85 mg/100 g oil; and further wherein the Df value, at a constant temperature, of the blended high oleic oil is improved when compared under the same conditions to art a comparable oil not comprising the high oleic soybean first oil and the second oil.
 19. The oil of any one of claims 3-18, wherein the oil comprises at least one antioxidant, selected from the group consisting of: tocopherols, tocotrienols, naturally occurring tocopherols, naturally occurring tocotrienols, Lubrizol 7653, TBHQ, Decanox MPS-90, natural plant extracts, or a combination thereof.
 20. The dielectric material of claim 1, wherein the material is woven.
 21. The dielectric material of claim 1, wherein the material is non-woven.
 22. The dielectric material of claim 1, wherein the material comprises aramid, polyimide, polyphenylsulfone, polyamide, polyester or polyethylene.
 23. The blended high oleic oil of claim 3, wherein the tocopherol is a naturally occurring tocopherol.
 24. The blended high oleic oil of claim 18, wherein the tocopherol is a naturally occurring tocopherol.
 25. The blended high oleic oil of claim 3, wherein the water content is less than about 300 ppm.
 26. The blended high oleic oil of claim 18, wherein the wherein the water content is less than about 300 ppm.
 27. A method comprising introducing the blended high oleic oil of claim 3 into a device for the generation, storage, conversion, or distribution of electrical energy.
 28. A method comprising introducing the blended high oleic oil of claim 18 into a device for the generation, storage, conversion, or distribution of electrical energy.
 29. A method comprising introducing the blended high oleic oil of claim 8 into a device for the generation, storage, conversion, or distribution of electrical energy.
 30. A method comprising introducing the blended high oleic oil of claim 10 into a device for the generation, storage, conversion, or distribution of electrical energy.
 31. A method for preconditioning a heat-transfer dielectric fluid, the method comprising exposing a heat-transfer dielectric fluid comprising the blended high oleic oil of claim 3 to a constant and uniformly distributed electromagnetic field.
 32. A method for preconditioning a heat-transfer dielectric fluid, the method comprising exposing a heat-transfer dielectric fluid comprising the blended high oleic oil of claim 18 to a constant and uniformly distributed electromagnetic field.
 33. The method of claim 31, wherein the electromagnetic field is applied in the form of microwaves.
 34. The method of claim 32, wherein the electromagnetic field is applied in the form of microwaves.
 35. The method of claim 31, wherein the electromagnetic field is applied at sufficient power and for a sufficient period of time to heat the vegetable triacylglycerol to about 140° C.
 36. The method of claim 32, wherein the electromagnetic field is applied at sufficient power and for a sufficient period of time to heat the vegetable triacylglycerol to about 140° C. 